Postgraduate
student Dubovkina I.
The Institute of Engineering Thermophysics of National Academy of Sciences of Ukraine
How to increase
the power efficiency in the technological lines of spray drying
Increase of efficiency of productions - large
consumers of heat energy, can be
reached by recycling of their waste energy.
Owing to intensive increase of the prices for energy
carriers the great value is got by problems connected with rational use of
energy and active methods of use of scientific and technical achievements which
provide production improvement of quality at saving use of fuel at the expense
of use of secondary resources.
Spray drying, being a component of many technologies, is
among the most power-intensive
technologies.
The
spray drying method, thanks to extremely developed surface of contact of
phases, is one of the most intensive and quickly proceeding methods of dehydration of liquid materials and
products. At spray drying processes diameters of drops make tens
micron that causes except a considerable surface of evaporation (1liter of the
solution with the diameter of drops 40 micron has evaporation surface 150м2 ) as well high intensity moisture
exchange, thanks to the big difference of temperatures (150-2000С)
between the heat-transfer
agent and a material.
At
the same time in comparison with other methods of drying the given method is
more power expenditure, because of use of
considerable volumes of the heat-transfer agent for realization of process of
drying sprayed product in volume of the chamber.
In respect of economy of power resources
sharply there is a question of decrease in losses of heat and reduction of
power inputs in heat - and mass-transfer the devices used for spray
drying of disperse materials as process spray drying is one of the most
power-intensive technological processes. In view of necessity of transfer of
water from liquid in a vaporous condition, and also use of great volumes of the
high-temperature heat-transfer agent process realization of spray drying demands considerable power expenses.
From the analysis of power expenses spray drying chamber of industrial technological lines follows, that the
greatest losses of heat are caused exhaust in a drying
process heat-transfer agent and heat losses in environment (fig. 1).
Thus, there are obvious basic ways of increase of heat
profitability spray drying installations:
- to reduce losses of
heat with exhaust
in a drying process heat-transfer agent (or rational use of this kind of waste energy);
1
- losses with exhaust in a drying process heat-transfer agent; 2 - losses with
flying steam; 3 - losses with a dried up material; 4 - other expenses;
Figure
1 – Distribution of power expenses in industrial technological lines of spray
drying.
- to reduce losses in environment.
Declining of
power losses and increasing of power efficiency in the technological lines of
the spray drying it can be attained for an account:
- utilizations of heat of waste gases from autonomous
heat-generator for the previous heating of heat-transfer agent;
- utilizations of heat
of exhaust in a drying process heat-transfer agent.
The
realization of measures of similar type needs, as a rule, creation and
designing of utilization or technological equipment.
For recuperation heat in technological processes usually use plate-type
heat exchangers, rotary heat exchangers (recuperators), run-around coils, and also recuperators on heat pipes [1].
The advantages of using heat pipes over conventional methods is
that large quantities of heat can be transported through a small
cross-sectional area over a considerable distance with no additional power
input to the system, (except for the fans to drive the airstreams) together
with simplicity of design and ease of manufacture [2], [3]. The device contains rows of finned tubes partially filled with refrigerant
and permanently sealed. Heating one side of a heat pipe establishes a
continuous process within it whereby the warmer side acts as an evaporator and
the colder side a condenser [4].
Preliminary
there was investigated a possibility of the using in the capacity of a
recuperator on the heat pipes of serial heat-exchange vehicles of type «freon – air», which are used in a refrigeration technique and equipment
on the pilot spray drying plant of The Institute of Engineering Thermophysics of
National Academy of Science of
Ukraine.
Hereafter the
work of industrial prototype of heat utilizer, on one of the plant of Ukraine
will test during the utilization of waste gases from autonomous heat-generator,
that provides work of the spray drying unit.
Bibliography:
1. O. G. Burdo, I.
V. Bezbah Rotating heat pipes in devices for heat treatment of the food- stuffs
// Applied Thermal Engineering 28 (2008) 341-343.
2. Leonard L. Vasiliev. Heat pipes in modern
heat exchangers // Applied Thermal Engineering. – 2005. – № 25. – P. 1–19.
3. Casarosa C., Latrofa E., Shelginski A. The
geyser effect in a two phase thermo-syfone // Int. Gournal of Heat and Mass
Transfer. V. 26. 1983. № 6. P.933–941.
4. Shelghinski A. Tubi di calore a media temperatura.
// ATTI del XXXVI Congresso Nazionale ATI dell Associazione Termotecnica
Italiana. Volume Viaregio: 1981. P. 739–752.